GB1483327A - Extraction of sugar from molasses - Google Patents
Extraction of sugar from molassesInfo
- Publication number
- GB1483327A GB1483327A GB1610876A GB1610876A GB1483327A GB 1483327 A GB1483327 A GB 1483327A GB 1610876 A GB1610876 A GB 1610876A GB 1610876 A GB1610876 A GB 1610876A GB 1483327 A GB1483327 A GB 1483327A
- Authority
- GB
- United Kingdom
- Prior art keywords
- resin
- molasses
- resin type
- per cent
- cation exchangers
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B35/00—Extraction of sucrose from molasses
- C13B35/02—Extraction of sucrose from molasses by chemical means
- C13B35/06—Extraction of sucrose from molasses by chemical means using ion exchange
Abstract
1483327 Extraction of sugar from molasses BAYER AG and SUDDEUTSCHE ZUCKER-AG 21 April 1976 [24 April 1975] 16108/76 Heading C6B Molasses is separated into sugars and non-sugar constituents by ion exclusion or liquid distribution chromatography on acid cation exchangers based on cross-linked copolymers of monovinyl compounds and divinyl compounds, in which the cation exchangers used are two different resin types A and B, whereof resin type A is a macroporous, acid cation exchanger which contains 8 to 20 wt. per cent of polyvinyl compounds and has an inner surface area of 5 to 150 m2/g of solids, whilst resin type B is an acid cation exchanger in the form of a gel, which contains from 2 to 6 wt. per cent of polyvinyl compounds and in which these resin types are so arranged in a separating column, or in several separating columns arranged in series, that the molasses to be separated first flow through resin type A, and that resin type A accounts for 5 to 35% by volume of the total resin through which the molasses flow. Resin type A may contain 30 to 50 wt. per cent of swelling water and resin type B may contain 55 to 65 wt. per cent of swelling water. The cation exchangers of types A and B may be present in the salt e.g. potassium, sodium, calcium, iron or aluminium form. Preferably the total volume of the bed of the cation exchangers is divided amongst two or more columns arranged in series. Resin types A and B are preferably strongly acid cation exchangers. The separation may be carried out at from 50 to 99‹C.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19752518284 DE2518284C2 (en) | 1975-04-24 | 1975-04-24 | MOLASSES DESUGUGAR |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1483327A true GB1483327A (en) | 1977-08-17 |
Family
ID=5944925
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1610876A Expired GB1483327A (en) | 1975-04-24 | 1976-04-21 | Extraction of sugar from molasses |
Country Status (7)
Country | Link |
---|---|
BE (1) | BE840992A (en) |
DE (1) | DE2518284C2 (en) |
DK (1) | DK183776A (en) |
FR (1) | FR2308685A1 (en) |
GB (1) | GB1483327A (en) |
LU (1) | LU74820A1 (en) |
NL (1) | NL7604222A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8003352B2 (en) | 2004-07-16 | 2011-08-23 | Iogen Energy Corporation | Method of obtaining a product sugar stream from cellulosic biomass |
US8247200B2 (en) | 2007-01-25 | 2012-08-21 | Iogen Energy Corporation | Method of obtaining inorganic salt and acetate salt from cellulosic biomass |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE202011109498U1 (en) | 2011-12-27 | 2012-02-13 | Franz Haimer Maschinenbau Kg | Tool holder and clamping system with such a tool holder |
WO2014190477A1 (en) * | 2013-05-28 | 2014-12-04 | Rohm And Haas Company | Removing impurities from sugar solutions |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1209978A (en) * | 1957-06-05 | 1960-03-04 | Rohm & Haas | Sugar manufacturing process |
US2937959A (en) * | 1958-10-23 | 1960-05-24 | Illinois Water Treat Co | Purification of sugar solutions by molecular exclusion |
US3174876A (en) * | 1963-03-06 | 1965-03-23 | John B Stark | Process for separating sugars |
GB1411455A (en) * | 1972-06-29 | 1975-10-22 | Pfeifer & Langen | Method of extracting sugar from molasses by the ion exclusion method |
-
1975
- 1975-04-24 DE DE19752518284 patent/DE2518284C2/en not_active Expired
-
1976
- 1976-04-21 GB GB1610876A patent/GB1483327A/en not_active Expired
- 1976-04-21 NL NL7604222A patent/NL7604222A/en not_active Application Discontinuation
- 1976-04-22 LU LU74820A patent/LU74820A1/xx unknown
- 1976-04-22 BE BE166356A patent/BE840992A/en not_active IP Right Cessation
- 1976-04-23 DK DK183776A patent/DK183776A/en unknown
- 1976-04-23 FR FR7612157A patent/FR2308685A1/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8003352B2 (en) | 2004-07-16 | 2011-08-23 | Iogen Energy Corporation | Method of obtaining a product sugar stream from cellulosic biomass |
US8247200B2 (en) | 2007-01-25 | 2012-08-21 | Iogen Energy Corporation | Method of obtaining inorganic salt and acetate salt from cellulosic biomass |
Also Published As
Publication number | Publication date |
---|---|
LU74820A1 (en) | 1977-02-07 |
DE2518284C2 (en) | 1977-05-18 |
FR2308685B1 (en) | 1980-12-05 |
FR2308685A1 (en) | 1976-11-19 |
NL7604222A (en) | 1976-10-26 |
DE2518284B1 (en) | 1976-09-16 |
BE840992A (en) | 1976-10-22 |
DK183776A (en) | 1976-10-25 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PCNP | Patent ceased through non-payment of renewal fee |